Field of the Invention
[0001] The present invention relates to the field of enzyme engineering, and in particular
to an α-amylase variant and use thereof.
Background of the Invention
[0002] In the industry, the hydrolysis of starch starts mainly with α-amylase. The combined
application of α-amylases derived from microorganisms and other enzyme species, such
as pullulanase, glucoamylase and glucose isomerase, can effectively break down starch
macromolecules, and the produced small-molecule polysaccharides or monosaccharides
are of great importance in many applications in food manufacturing, grain processing,
beer processing, and alcohol production. The α-amylase belongs to saccharifying hydrolase,
with a main structural feature of (α/β)8 folding, which contains a special starch
substrate binding site with a length of generally no more than 10 saccharide monomers.
However, the binding sites of several amylases can work together to perform multi-site
binding to successfully cleave starch macromolecules.
[0003] The α-amylase can effectively cleave the α-1,4 glycosidic bond in the starch substrate,
thereby rapidly reducing molecular weight and viscosity of the starch substrate, and
the products are mainly dextrins of different lengths. There are different kinds of
α-amylases, and industrial application conditions of these kinds of α-amylases vary
greatly depending on the characteristics of the desired products.
[0004] The α-amylase (α-1,4-glucan-4-glucanohydrolases, E.C. 3.2.1.1) is effective in hydrolyzing
the α-1,4 glycosidic bond in starch and other polysaccharides. In view of the demand
for improving enzyme efficiency and reducing production cost during the hydrolysis
of starch, the search for α-amylase which can support effective starch liquefaction
in different application fields has become an important research area in the academia
and industry. At present, the improvements of the enzyme species by using enzyme engineering
techniques mainly focus on the improvements of heat resistance, acid-base tolerance
performance, and liquefaction effect.
[0005] Many α-amylases in plants and microorganisms have been found to have commercial values,
mainly including
B. licheniformis α-amylase,
B. amyloliquefaciens α-amylase and
G.
stearothermophilus α-amylase, wherein the variants derived from
B. licheniformis α-amylase as a template are the most abundant and are most widely used.
[0006] In the present invention, in order to meet the needs of industrial production, we
used
G.
stearothermophilus α-amylase as a template to construct a series of α-amylase variants, and improved
the application efficiency of the enzyme species. Especially when pH is low and the
amount added is reduced, the liquefaction efficiency of the α-amylase variants of
the present invention can be comparable to that of the mainstream products in the
market.
Summary of the Invention
[0007] An object of the present invention is to provide a series of
G.
stearothermophilus α-amylase variants, which can increase the liquefaction efficiency and can adapt
to the needs of industrial production. In particular, the enzyme activity and other
properties of the α-amylase variants of the present invention can be comparable to
those of mainstream products in the market under the conditions of a temperature of
100°C or above and a pH of 5.0.
[0008] Another object of the present invention is to provide a gene encoding the α-amylase
variant.
[0009] Still another object of the present invention is to provide a method for producing
the α-amylase variant and use thereof.
[0010] The objects of the present invention can be achieved by the following technical solutions:
An α-amylase variant, which is obtained by mutating or deleting at least one amino
acid residue in amino acid sequence of a parental α-amylase, while still retaining
the ability of the parental α-amylase to hydrolyze an α-1,4 glycosidic bond; and has
amino acid sequence homology of 95% or more with the parental α-amylase.
[0011] The parental α-amylase is preferably a natural α-amylase, i.e. a bacterial α-amylase,
more preferably an α-amylase of any one selected from the group consisting of
Bacillus subtilis, B. licheniformis, B. amyloliquefaciens, G. stearothermophilus or
Bacillus cereus, further more preferably an α-amylase of
B. licheniformis or
G. stearothermophilus, and most preferably an α-amylase of
G. stearothermophilus.
[0012] The full-length gene sequence encoding the α-amylase
of G. stearothermophilus is set forth in SEQ ID NO: 1; and the corresponding amino acid sequence is set forth
in SEQ ID NO: 2.
[0013] The α-amylase variant is preferably obtained by any one of the following, or any
combination of the following:
- (1) deleting the 1st to 5th amino acid residues from the N-terminus of the parental α-amylase of G. stearothermophilus and replacing with VN or ANLN;
- (2) deleting 27 to 32 amino acid residues from the C-terminus of the parental α-amylase
of G. stearothermophilus; for example, deleting the 1st to 27th amino acid residues from the C-terminus; or deleting the 1st to 29th amino acid residues from the C-terminus; or deleting the 1st to 32nd amino acid residues from the C-terminus;
- (3) deleting the 180th and 181st amino acid residues from the N-terminus of the parental α-amylase of G. stearothermophilus.
[0014] The α-amylase variant is further preferably to be added with three amino acid residues
of FAN at the C-terminus in addition to any one of above three cases or any combination
of the three cases.
[0015] The amino acid sequence of the α-amylase variant is further preferably any one selected
from the group consisting of SEQ ID NO: 4, SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO:
10 and SEQ ID NO: 12.
[0016] The nucleotide coding sequence of the α-amylase variant is any one selected from
the group consisting of SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9 and
SEQ ID NO: 11.
[0017] A gene encoding the α-amylase variant of the present invention is provided.
[0018] Wherein, the gene is preferably any one selected from the group consisting of SEQ
ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9 and SEQ ID NO: 11.
[0019] There is provided an expression vector for expressing the α-amylase variant of the
present invention, which comprises a gene encoding the α-amylase variant according
to claim 8.
[0020] Wherein, the expression vector comprises an expression cassette comprised mainly
of a natural or synthetic promoter sequence, a natural or synthetic ribosome binding
site, a natural or synthetic terminator sequence, and the gene sequence encoding the
α-amylase variant of the present invention.
[0021] There is provided a recombinant cell for expressing the α-amylase variant of the
present invention, which comprises one or more genes encoding the α-amylase variant
of the present invention.
[0022] Wherein, the host cell of the recombinant cell is preferably selected from a
Bacillus strain, further preferably
B. licheniformis or a
Bacillus strain genetically engineered to inactivate some endogenous proteins; most preferably
B. licheniformis genetically engineered to inactivate AprE and/or NprE.
[0023] There is provided a method for producing the α-amylase variant of the present invention,
which comprises the steps of: culturing a recombinant cell containing a gene sequence
encoding the α-amylase variant under conditions suitable for the expression of the
α-amylase variant, and obtaining the α-amylase variant from the recombinant cell or
its culture supernatant.
[0024] Also provided is the use of the α-amylase variant of the present invention in hydrolysis
of an α-1,4 glycosidic bond of a polysaccharide; preferably in hydrolysis of an α-1,4
glycosidic bond of a polysaccharide under conditions of a high temperature and/or
a low pH.
[0025] Wherein, the high temperature is preferably 80°C to 110°C, more preferably 100°C
to 110°C, and the low pH is preferably 5.0 to 5.5.
Beneficial Effects
[0026] A series of α-amylase variants provided by the present invention have high catalytic
activity under an acidic condition of pH 5.0 and a high temperature of 100°C or above.
The acid resistance and thermal stability of these α-amylase variants are suitable
for starch liquefaction.
Brief Description of the Drawings
[0027]
FIG. 1 shows a pYF-tsDE vector, which comprises a temperature-sensitive element (having
replication activity at 30°C) and an erythromycin determinant gene (ErmC), which can
tolerate 300 µg/mL erythromycin in E. coli and 5 µg/mL erythromycin in B. licheniformis. The recombinant host cell containing the nucleotide sequence encoding the α-amylase
variant was screened with erythromycin.
FIG. 2 is a schematic diagram of a pUC57-KS-erm vector from which the pYF-tsDE vector
of the present invention can be obtained.
FIG. 3 is a schematic diagram of a pYF-tsINT-amy vector.
Figure 4 shows the protein flocculation and viscosity.
Figure 5 is a graph showing the results of liquefaction experiments under different
starch slurry concentrations.
Figure 6 shows the results of acid resistance experiments of the α-amylase variants.
Detailed Description of the Invention
[0028] Unless otherwise specified, all technical and scientific terms used herein have the
same meanings as commonly understood by skilled persons. In this application, certain
terms have the same meanings as the specification describes. It must be noted that
as used herein and in the appended claims, the singular forms "a", "an", and "the"
may include plural forms unless the context clearly dictates otherwise.
[0029] In the present invention, the term "a-amylase" refers to an enzyme capable of hydrolyzing
an α-1,4 glycosidic bond of a polysaccharide. For example, the α-amylase can hydrolyze
starch to dextrin.
[0030] In the present invention, the term "parental α-amylase" refers to a natural α-amylase.
The natural α-amylase is a bacterial α-amylase and its source includes, but is not
limited to,
Bacillus subtilis, B. licheniformis, B. amyloliquefaciens, G stearothermophilus and
Bacillus cereus.
[0031] According to a preferred embodiment of the present invention, the natural α-amylase
is derived from a
Bacillus strain, especially
B. licheniformis and
G.
stearothermophilus. The full-length encoding sequence of the α-amylase of
G stearothermophilus is set forth in SEQ ID NO: 1, and the corresponding amino acid sequence is set forth
in SEQ ID NO: 2.
[0032] In the present invention, the term "a-amylase variant" refers to a non-naturally
occurring α-amylase obtained by mutation or deletion of one or several amino acid
residues in the amino acid sequence of the parental α-amylase, while still retaining
the ability of the parental α-amylase to hydrolyze an α-1,4 glycosidic bond.
[0033] In the present invention, the term "liquefaction" generally refers to the process
of breaking down carbohydrates into small molecule polysaccharides. When an α-amylase
or α-amylase variant is added, "liquefaction" specifically refers to hydrolyzing the
α-1,4 glycosidic bond of the carbohydrate.
[0034] In the present invention, the term "α-1,4 glycosidic bond" refers to a bond linking
C1 of the former glucose with C4 of the latter glucose, that is, an α-1,4 glycosidic
bond.
[0035] The present invention relates to an "a-amylase variant" obtained by sequence modification
of a parental α-amylase. The parental α-amylase is a natural α-amylase, particularly
a natural α-amylase derived from bacteria. According to an embodiment of the present
invention, an α-amylase variant is obtained by the mutation or deletion of one or
several amino acid residues in the amino acid sequence of the parental α-amylase.
[0036] The present invention includes a series of α-amylase variants. According to an embodiment
of the present invention, the homology of the amino acid sequences of the series of
α-amylase variants is at least 95%, even 95%, 96%, 97%, 98%, 99% or 100%, respectively.
[0037] As an illustrative and non-limiting example of the invention, the α-amylase variant
is obtained by any one of the following:
- (1) deleting the 1st to 5th amino acid residues from the N-terminus and replacing with VN, and deleting the 1st to 27th amino acid residues from the C-terminus of the parental α-amylase of G. stearothermophilus, with an amino acid sequence as set forth in SEQ ID NO: 4.
- (2) deleting the 1st to 5th amino acid residues from the N-terminus and replacing with ANLN, deleting the 180th and 181st amino acid residues from the N-terminus, and deleting the 1st to 27th amino acid residues from the C-terminus of the parental α-amylase of G. stearothermophilus, with an amino acid sequence as set forth in SEQ ID NO: 6.
- (3) deleting the 1st to 5th amino acid residues from the N-terminus and replacing with ANLN, deleting the 180th and 181st amino acid residues from the N-terminus, and deleting the 1st to 29th amino acid residues from the C-terminus of the parental α-amylase of G. stearothermophilus, with an amino acid sequence as set forth in SEQ ID NO: 8.
- (4) deleting the 1st to 5th amino acid residues from the N-terminus and replacing with ANLN, deleting the 180th and 181st amino acid residues from the N-terminus, and deleting the 1st to 32nd amino acid residues from the C-terminus of the parental α-amylase of G. stearothermophilus, with an amino acid sequence as set forth in SEQ ID NO: 10.
- (5) deleting the 1st to 5th amino acid residues from the N-terminus and replacing with ANLN, deleting the 180th and 181st amino acid residues from the N-terminus, deleting the 1st to 27th amino acid residues from the C-terminus, and adding three amino acid residues of
FAN at the C-terminus of the parental α-amylase of G. stearothermophilus, with an amino acid sequence as set forth in SEQ ID NO: 12.
[0038] The amino acid sequence of the α-amylase variant is any one selected from the group
consisting of SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 10 and SEQ ID NO: 12.
[0039] The α-amylase variant of the present invention retains the ability to hydrolyze the
α-1,4 glycosidic bond. In addition, the performance of these α-amylases meets the
requirements of industrial production, such as the improvement of liquefaction efficiency,
and the stable catalytic activity at an acidic pH or a high temperature.
[0040] According to an embodiment of the present invention, the α-amylase variant is stable
in catalytic activity at an acidic condition of pH 5.0 or at a temperature of 100°C
or above (especially at a temperature between 100°C and 110°C). The improved properties
of the α-amylase variant are more amenable to the liquefaction reactions in the starch
industry, because the liquefaction process in the starch industry is often carried
out at conditions of a low pH and a high temperature.
[0041] All α-amylase variants of the present invention can be used in the liquefaction reaction.
In a preferred embodiment, the α-amylase variant is derived from a parental α-amylase,
in particular a parental α-amylase derived from
G.
stearothermophilus. In a particularly preferred embodiment, the amino acid sequence of the α-amylase
variant is set forth in any one of SEQ ID NO: 4, SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID
NO: 10 and SEQ ID NO: 12.
[0042] According to the present invention, any carbohydrate containing α-1,4 glycosidic
bond can be used in the liquefaction reaction. The carbohydrates containing one or
more α-1,4 glycosidic bonds include but are not limited to starch, amylopectin, amylose,
and dextran.
[0043] Many carbohydrates contain an α-1,6-glycosidic bond and an α-1,4-glycosidic bond,
such as amylopectin. The term "α-1,4-glycosidic bond" refers to a bond linking C1
of the former glucose with C4 of the latter glucose, that is, an α-1,4 glycosidic
bond. Therefore, the α-amylase variant of the present invention can be used in conjunction
with a pullulanase capable of hydrolyzing an α-1,6 glycosidic bond during saccharification.
The enzymes capable of hydrolyzing an α-1,4 glycosidic bond include, but are not limited
to, α-amylases. In a preferred embodiment of the present invention, the enzyme that
catalyzes the hydrolysis of an α-1,4 glycosidic bond is an α-amylase.
[0044] Therefore, according to an embodiment of the present invention, a method for further
catalyzing the saccharification reaction to increase the efficiency is to use pullulanase
in combination. In the present invention, the term "pullulanase" refers to a hydrolase
capable of hydrolyzing an α-1,6 glycosidic bond.
[0045] The use of the α-amylase of the present invention in combination with pullulanase
in the saccharification of starch can increase the purities of glucose and maltose.
In addition, the use of the aforementioned complex enzyme in the saccharification
reaction can effectively reduce the substrate concentration, increase the conversion
efficiency, and can also have a higher catalytic activity at an acidic pH or a higher
temperature, and can be more adapted to industrial conditions for hydrolyzing starch.
[0046] The present invention provides a method in which an α-amylase variant can hydrolyze
an α-1,4 glycosidic bond for saccharification under any temperature and pH conditions
suitable for industrial production. According to the present invention, the liquefaction
reaction can be carried out at a high temperature of 80°C to 110°C, such as 80°C,
90°C, 100°C, 105°C, and 110°C. The saccharification reaction can also be carried out
under an acidic pH condition of pH 5.0 to pH 5.5, such as pH 5.0, 5.1, 5.2, 5.3, 5.4,
and 5.5.
[0047] According to an embodiment of the present invention, the catalytic activity is stable
in the liquefaction reaction catalyzed by an α-amylase variant under conditions of
an acidic pH and a temperature of 100°C or above.
[0048] In another aspect, the expression vector of the present invention comprises a synthetic
nucleotide sequence encoding an α-amylase variant, and a recombinant host cell comprises
the above expression vector. The expression vector may comprise a series of synthetic
nucleotide sequences encoding different α-amylase variants. The expression vector
can be integrated into the genome of the host cell. For example, the expression vector
may comprise the synthetic nucleotide sequence SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID
NO: 7, SEQ ID NO: 9 and SEQ ID NO: 11.
[0049] The expression vector of the present invention preferably comprises a natural or
synthetic promoter sequence, a natural or synthetic ribosome binding site, and a natural
or synthetic terminator sequence. These genetic elements together with the encoding
sequence of the synthetic α-amylase variant constitute an expression cassette, which
constitutes an expression vector together with a vector backbone. For example, the
expression vector comprises an expression cassette which includes the following elements:
a promoter sequence, a synthetic ribosome binding site, a synthetic nucleotide sequence
encoding an α-amylase variant of the present invention and a terminator sequence.
A signal sequence is capable of directing the secretion of the α-amylase variant,
and the introduction of the signal sequence into the expression vector or expression
cassette, especially the introduction of the signal sequence upstream of the start
codon is more advantageous for the secretion of the α-amylase variant.
[0050] According to a preferred embodiment of the present invention, the expression vector
is suitably expressed in bacteria, in particular a
Bacillus strain, and more preferably expressed in
B. licheniformis. In a particularly preferred embodiment, the expression vector can be integrated into
the genome of
Bacillus, in particular the genome of
B. licheniformis. The expression vector for a host cell that can be used for integration of polynucleotide
sequences in chromosome and a method for constructing such an expression vector are
well-known common skills in the field of contemporary biology.
[0051] According to an embodiment of the present invention, the recombinant host cell may
be genetically engineered to comprise one or more nucleic acid sequences encoding
α-amylase variant. Any technique can be used to genetically engineer a host cell to
comprise one or more synthetic nucleic acid sequences encoding the α-amylase variant
of the present invention, e.g., chromosomal integration. A vector containing a temperature-sensitive
origin and a resistance selection marker can be used for the integration step. The
vector is integrated with a specific region of the genome through the Campbell mechanism,
and a recombinant strain is obtained through resistance screening. The resistance
screening marker of the recombinant strain is removed by homologous recombination
during the subsequent cultivation.
[0052] According to an embodiment of the present invention, the recombinant host cell has
been engineered to inactivate some endogenous proteins. The endogenous proteins that
can be inactivated include, but are not limited to, extracellular proteases. Some
endogenous proteins are inactivated either before or after the recombinant host cell
is transformed with a nucleic acid sequence containing an α-amylase variant expressing
gene. A more suitable method is to inactivate the exogenous secreted protease of the
host bacterium before transferring the vector of the α-amylase variant expressing
gene.
[0053] First,
B. licheniformis has been modified to inactivate some exogenous protease genes. In particular, some
extracellular proteases, such as subtilisin (AprE), glutamic acid-specific protease
(Blase) can be inactivated in the
B. licheniformis strain. The genetic engineering makes the
B. licheniformis strain more suitable for the expression and secretion of an α-amylase variant.
[0054] The present invention provides a method for producing an α-amylase variant. According
to an embodiment of the present invention, the method comprises culturing a recombinant
host cell containing a nucleotide sequence encoding an α-amylase variant under conditions
suitable for the expression of an α-amylase variant and obtaining the α-amylase variant
from the recombinant host cell or its supernatant.
[0055] All recombinant host cells of the present invention are capable of producing α-amylase
variants. The recombinant host cell comprises at least one copy of a nucleotide sequence
encoding an α-amylase variant. The nucleotide sequences encoding an α-amylase variant
is capable of expressing the α-amylase variant under suitable conditions. The α-amylase
variant secreted from the recombinant host cell can be collected from the recombinant
cell or supernatant. The collection method includes but is not limited to filtration,
centrifugation, and the like.
[0056] According to an embodiment of the present invention, an α-amylase variant can be
produced in large amount by fermentation of genetically engineered
B. licheniformis. The nucleotide sequence encoding the α-amylase variant is introduced into
B. licheniformis by genetic engineering. More preferably,
B. licheniformis of the present invention has been modified to remove the resistance screening gene
and is environmentally friendly, and the produced α-amylase variant is more suitable
for use in the food industry.
[0057] The following examples of the present invention further illustrate the essence of
the present invention. It should be understood that the following examples do not
limit the present invention, and the scopes of the present invention are determined
by the appended claims.
Examples
Example 1: Construction of pYF-tsDE plasmid
[0058] pYF-tsDE (FIG. 1) was a thermosensitive
E.coli/
B. licheniformis shuttle plasmid. The plasmid comprised a temperature-sensitive replication origin
(being active at 30°C) and an erythromycin resistance gene (ErmC), the resistance
of which was 300 µg/ml in
E. coli, and 5 µg/ml in
B. licheniformis. At 37°C, the replication origin on the plasmid was inactivated and the plasmid was
integrated into the specified site of the host genome and screened with ErmC.
[0059] The pYF-tsDE plasmid was constructed by digesting the plasmid pUC57-KS-erm (synthesized
by Genscript with commission, and the sequence was shown in
CN 104073458A, FIG. 2) with BglII, recovering, purifying a 3.8 kbp fragment and self-ligating with
T4 ligase (New England Biolabs), and the cloned plasmid was pYF-tsDE. Transformants
were propagated in
E. coli TOP10 and served as the backbone for all of the following gene manipulations.
Example 2: Construction of a protease deficient B. licheniformis strain
[0060] Genetically engineered strains that are host cells for recombinant enzyme products
have been reported in the literature (
Widner et al., Journal of Industrial Microbiology & Biotechnology, 25, 204-212, 2000). These recombinant host cells typically contain one or more nucleic acid structures
coding a target sequence for expression of an enzyme. In the present invention,
B. licheniformis is used as a genetically manipulated recipient bacterium. The transformation of
Bacillus can now be achieved through very mature means such as competent cell transformation,
electrotransformation and protoplast transformation (
Young et al., J Bacteriology, 81, 823-829, 1961;
Shigekawa et al., Biotechniques, 6, 742-751, 1988;
Chang et al., Molecular General Genetics, 168, 111-115, 1979).
[0061] In the present invention, a single expression cassette for α-amylase variant comprised
a natural or synthetic promoter sequence, a signal peptide sequence screened from
Bacillus, a synthetic ribosome binding site, and an α-amylase variant coding gene from
G.
stearothermophilus, and a transcription terminator. Such a design would greatly enhance the level of
gene expression in the host strain and the secretion amount of the α-amylase variant.
Replacing a specific site on the genome of the
B. licheniformis cell with the α-amylase variant coding gene was achieved by plasmid-mediated single
cross-homologous recombination.
[0062] In
B. licheniformis, the activities of extracellular proteases are detrimental to the secretion of heterologous
enzymes. Two major extracellular proteases have been identified: subtilisin (AprE)
and glutamic acid-specific protease (Blase). Most of the extracellular protease activities
in
B. licheniformis originate from these two proteases.
[0063] In the present invention, in order to obtain the structural integrity of the α-amylase
variant gene, the above two genes were inactivated, and the continuous cross single
Campbell type mechanism was adopted. The specific operation was as follows:
2.1 pYF-tsDE was digested by BglII and treated with CIP to inhibit self-ligation;
2.2 Gene knockout
[0064]
- (1) In order to obtain each gene deletion fragment, a homologous sequence of approximately
500 bp was respectively amplified from each side of the gene to be deleted by PCR
using the genomic DNA of B. licheniformis (CICC 22794, purchased from the China Center of Industrial Culture Collection) as
a template. The monoclonal B. licheniformis was pre-denatured at 98°C for 5 minutes and could be used directly as a genomic DNA
template in a PCR reaction.
[0065] The primers used for the PCR reaction were synthesized by Genscript. The primer sequences
were as follows:
The primers for amplifying the upstream sequence of the Apr gene were:
| lichApr_F1 |
TTATTGAGCGGCAGCTTCGACATTGATCAGACCTT |
| lichApr_R1 |
CCTTACGGCATTCCTCTCAACAGCGGATCTTCAG |
The primers for amplifying the downstream sequence of the Apr gene were:
| lichApr_F2 |
CCTGAAGATCCGCTGTTGAGAGGAATGCCGTAAGG |
| lichApr_R2 |
ATGATGAGGAAAAAGAGTTTTTGGCTTGGGATGCTGAC |
The primers for amplifying the upstream sequence of the Blase gene were:
| blalich_F1 |
TTATTGTGCGCTGTTTTTCCAGTTGGTCAAATTGTCG |
| blalich_cR1 |
CGGACAAGGGTCACCAACGGGACAACTGTTACCATC |
The primers for amplifying the downstream sequence of the Blase gene were:
| blalich_cF2 |
GATGGTAACAGTTGTCCCGTTGGTGACCCTTGTCC |
| blalich_R2 |
CGGCGTTGGTTAGTAAAAAGAGTGTTAAACGAGGTTTGAT |
The PCR amplification system was 50µl and the reaction procedure was as follows:
- (1) monoclonal B. licheniformis 14580 pre-denatured at 98°C for 8 minutes;
- (2) 96°C, 15 seconds;
- (3) 58°C, 15 seconds;
- (4) 72°C, 30 seconds; steps 2-4 repeated for 25-30 times;
- (5) Final extension at 72°C, 2 minutes.
[0066] The PCR product was detected by 0.8% agarose gel electrophoresis and purified using
an Axygen kit.
2.3 Amplification of a target gene with an internal deletion of approximately 400-500
bp in the sequence by overlap extension PCR method
[0067] The internal gene deletion fragment was obtained using overlap extension PCR (SOE).
The specific operation was as follows:
- (1) The upstream and downstream PCR fragments of each gene in 2.2 were recovered and
purified;
- (2) Using the upstream and downstream homologous fragments of each gene of interest
in 1:1 molar ration as template, PCR amplification was performed using primers XX-CZ-F1
and XX-CZ-R2 ("XX" for Apr or Blase) to obtain the AprE gene or Blase gene with internal
fragments deleted.
[0068] The fragments were then recombined into the BglII-linearized pYF-tsDE vector using
a Clone-EZ Cloning Kit (provided by Genscript) and the resulting recombinant plasmids
were named: pYF-tsDE-Apr and pYF-tsDE-Blase. These recombinant plasmids were temperature-sensitive
plasmids, and the Apr gene or Blase gene contained therein lacks an internal sequence
of about 400-500 bp with respect to the intact gene, respectively.
[0069] Replacement of different alleles can be achieved by homologous recombination. The
method can be referred to
CN102124112A, and other well-known methods of homologous recombination in the art can also be
used.
2.4 Plasmid transformation
[0070] The method for transforming a knockout plasmid into competent cells of
B. licheniformis, and the screening process used in the experiment were as follows:
(1) The thermosensitive plasmid pYF-tsDE-Apr or pYF-tsDE-Blase was used to transform
B. licheniformis (CICC 22794, purchased from China Center of Industrial Culture Collection) competent
cells;
(2) Positive clone strains were screened with erythromycin (5 µg/ml) resistance on
LB (lOg of peptone, 5g of yeast extract, and 10g of sodium chloride per liter) medium
at 30°C;
(2) The positive clone strains were then transferred to condition of 37°C for incubation,
allowing the temperature-sensitive plasmid to be fused to the host genome. In order
to replace the gene at the preset position, several clones were selected and inoculated
in 2×YT medium for 24 hours, and then subcultured once. The whole process was subcultured
for 4-5 times (generally 5-7 days).
(3) Erythromycin-sensitive Bacillus subtilis cells were screened for PCR identification. The transparent hydrolysis circle could
be observed with a 1% skim milk LB plate at the same time. The knockout strain should
show a significantly reduced hydrolysis circle.
[0071] PCR primers used in the identification:
AprE: Apr-seqF1/Apr-seqR3
Blase: Blase-seqF1/Blase-seqR3
| Apr-seqF1: |
GCCAGGTTGAAGCGGTCTATTCAT |
| Apr-seqR3: |
TACGGCCATCCGACCATAATGGAAC |
| Blase-seqF1: |
GAAGAGCCGGTCACAATTGC |
| Blase-seqR3: |
GGCCGTTAGATGTGACAGCC |
Example 3: Integration and construction of α-amylase variant strain
3.1 Construction of amylase expression cassette
[0072] The integration plasmid was constructed using the same method as the pYF-tsDE plasmid
described above. In order to integrate the expression cassette into the designed AmyE
site on the genome, a homologous region of about 800 bp was respectively designed
upstream and downstream of the AmyE site on the genome and ligated on both sides of
an α-amylase variant expression cassette. At the same time, a number of completely
naturally selected bacterial chromosomal DNA fragments and functional synthetic sequences
were assembled, which were necessary for controlling the expression of the α-amylase
variant gene.
[0073] A typical amylase expression cassette comprised the following components. A typical
α-amylase variant expression cassette comprised the following elements: a natural
or synthetic promoter sequence (SEQ ID NO: 13), a synthetic ribosome binding site
aaaggagg, an α-amylase variant coding gene derived from
G.
stearothermophilus (SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9 or SEQ ID NO: 11, respectively)
and a synthetic terminator sequence (SEQ ID NO: 14). A strong natural signal sequence
(SEQ ID NO: 15) screened from
Bacillus subtilis was inserted upstream of the promoter of the α-amylase variant coding gene to enhance
the secretion efficiency of the expressed enzyme. The complete α-amylase variant expression
cassette was inserted into the BglII site in the linearized pYF-tsDE using a Clone-EZ
Cloning Kit (Genscript). The resulting temperature-sensitive integration plasmid was
named pYF-tsINT-amy (FIG. 3). The synthesis of the above sequence was performed by
Genscript, and the above sequences were sequentially tandemly connected to obtain
an α-amylase enzyme expression cassette. The signal peptide sequence in this cassette
was screened from
Bacillus subtilis and could effectively increase the secretion of α-amylase.
3.2 Plasmid Transformation
[0074] The entire α-amylase expression cassette (including homologous segments upstream
and downstream of the amyE gene) was circularized using a recombinant technique to
cyclize the BglII-linearized pYF-tsDE plasmid (recombination kit provided by Genscript),
and the constructed thermosensitive plasmid was named as pYF-tsINT-amy. The plasmid
was used for transformation into
Bacillus licheniformis with deletion of the AprE and Blase protease genes (CICC 22794, purchased from China
Center of Industrial Culture Collection), and the α-amylase variant expression cassette
without resistance marker was going to replace AmyE. Using the method described above,
a strain in which the α-amylase variant coding gene was successfully integrated into
the chromosome of
B. licheniformis produced a transparent circle on the blue starch plate, and PCR further confirmed
that the expression cassette was integrated in the AmyE site of the recipient strain.
[0075] The
B. licheniformis engineered strain that produced an α-amylase variant was stored at -80°C.
Example 4: Shake flask fermentation of α-amylase variant production
[0076] An activated bacterial monoclone (containing the α-amylase variant expression cassette)
was inoculated into 20 ml medium (containing maltose syrup 4.0%, peptone 2.0%, yeast
powder 0.1%, KH
2PO
4 0.6% and corresponding antibiotics) to log phase. 1.2 ml of the culture solution
was inoculated into 30 ml medium (containing maltose syrup 12.0%, peptone 1.0%, yeast
powder 1%, KH
2PO
4 0.2%, and MnCl
2 0.003%), and cultured on a reciprocating shaker at 120 rpm for 3 days. Samples were
taken at 24 hours, 48 hours and 72 hours, respectively, and centrifuged at 1000 rpm
for 1 minute. The supernatant was stored and analyzed by SDS-PAGE. The α-amylase variant
had a molecular weight of about 53 kD.
[0077] The α-amylase variant activity was measured as described in Example 6.
Example 5: Step-feeding fermentation process for α-amylase variant
[0078] The genetically engineered
B. licheniformis strain cryopreserved at -80°C obtained in Example 3 was streaked on an agar slant,
and cultured overnight at 37°C. The agar slant formula was as follows: peptone 1%,
yeast extract 0.5%, NaCl 1%, and agar powder 2%.
[0079] First, several fresh clones were selected and cultured in a seed shake flask containing
50 ml of culture medium at 37°C for 16 hours. Seed shake flask formula: maltose syrup
4.0%, peptone 2.0%, yeast extract 0.1%, and KH
2PO
4 0.6%. After 16 hours, all the seed broths were transferred to a 7 L stainless steel
fermenter containing 4 L of culture medium and the fermentation was continued for
12 hours at agitation speed of 350 rpm and an aeration rate of 650 L/H. Fermenter
formula: malt syrup 6.0%, peptone 1.0%, yeast extract 1%, KH
2PO
4 0.2%, and MnCl
2 0.003%. The fermentation pH was then controlled at about 5.7 ± 0.2 with 5% phosphoric
acid and the fermenter was continuously fed at a rate of 1 L/18 hrs in the first 18
hours and at a rate of 0.5 L/18 hrs for the next 110 hours. The feed formula was as
follows: maltose syrup 48%, peptone 6%, and yeast extract 8%. The entire fermentation
process lasted 140-150 hours. All media in the fermenter were collected and centrifuged
at 4°C, 1010 krpm for 30 minutes. The supernatant after centrifugation was used for
α-amylase variant enzymatic activity analysis.
Example 6: Amylase activity assay
[0080] The amylase activity assay was performed using Bestzyme amylase unit (BAU). One BAU
is defined as the amount of enzyme required to liquefy 1 mg of soluble starch in 1
minute at pH 6.0 and 70°C.
[0081] Briefly, the enzyme activity was determined as follows: 20 ml of 20 g/L soluble starch
solution was mixed with 5 ml of phosphate buffer pH 6.0, preheated at 70°C for 8 min,
then 1.0 ml of diluted enzyme solution was added, and the reaction was accurately
performed for 5 minutes. 1 ml of the reaction solution was added to a test tube containing
in advance 0.5 ml of 0.1 mol/L hydrochloric acid solution and 5 ml of dilute iodine
solution, and shaken well. With 0.5 ml 0.1 mol/L hydrochloric acid solution and 5
ml dilute iodine solution as a blank, the absorbance value was quickly measured at
a wavelength of 660nm, and the enzymatic activity of the test sample was obtained
by checking the table according to the absorbance.
Example 7: Application of amylase
[0082] All of the following results were based on the sequence of the α-amylase variant
SEQ ID NO: 8.
[0083] Unless otherwise stated, 1 BAU: the amylase activity assay was performed using Bestzyme
amylase unit (BAU). One BAU is defined as the amount of enzyme required to liquefy
1 mg of soluble starch in 1 minute at pH 6.0 and 70°C.
tDS: dry matter per ton
[0084] The amylase expressed and isolated from the
B. licheniformis cells was first subjected to a first round of liquefaction test using corn starch.
Test conditions: 18 Baume degrees (°Bé), well-mixed, pH adjusted to 5.2 with hydrochloric
acid. 0.22 kg/tDS of amylase was added, with a jetting temperature of 100°C, 105°C,
108°C, 110°C, and 115°C, respectively, maintained for 5 to 8 minutes followed by flashing
and then maintained at 95°C for 120 minutes. After liquefaction, the DE and iodine
tests were performed, and the protein flocculation and viscosity were observed. The
results are shown in Table 1 and FIG. 4.
Table 1: Comparison of amylase liquefactions at different jetting temperatures
| Temperature (°C) |
DE (%) |
| 100 |
17.64 |
| 105 |
14.91 |
| 108 |
10.62 |
| 110 |
10.21 |
| 115 |
3.06 |
[0085] The results showed that, at different jetting temperatures, the liquefaction at 100°C
was overdone; the liquefaction at 105°C was appropriate and the protein flocculation
was good; the liquefaction at 108°C and 110°C was still good and the protein flocculation
was normal, indicating that the α-amylase variant had good heat resistance, while
the liquefaction at 115°C was poor, indicating that the α-amylase variant could not
tolerate the high temperature of 115°C.
[0086] Secondly, we tested the resistance of the amylase to high substrate concentration
by liquefaction experiments with different starch slurry concentrations. The liquefaction
conditions were the same as those described above, and the jetting temperature was
108°C. The results are shown in Table 2 and FIG. 5.
Table 2: Comparison of amylase liquefactions at different concentrations of starch
slurry
| Baume degree (°Bé) |
DE (%) |
| 15 |
8.58 |
| 18 |
10.73 |
| 20 |
12.10 |
| 22 |
14.29 |
[0087] As shown in Table 2, at different starch slurry concentrations, the α-amylase variant
was still able to normally liquefy when the concentration of the starch slurry was
as high as 22°Bé, indicating that the α-amylase variant of the present invention could
be used for thick slurry liquefaction, thereby effectively saving factory costs.
[0088] Then, we measured the acid resistance of the amylase variant and performed liquefaction
with different amounts of enzyme added. The liquefaction reaction conditions were
as described above, the pH was 5.0, and the amount of enzyme added was 0.05, 0.1,
0.15, 0.2, 0.22, 0.25, and 0.3 kg/tDS, respectively. The results are shown in Table
3 and FIG. 6.
Table 3: Comparison of amylase liquefactions with different amounts of enzyme added
at pH 5.0
| Amount of enzyme added (kg/tDS) |
DE (%) |
| 0.05 |
3.41 |
| 0.10 |
6.18 |
| 0.15 |
8.04 |
| 0.20 |
8.12 |
| 0.22 |
9.81 |
| 0.25 |
10.41 |
| 0.30 |
11.77 |
[0089] As shown in Table 3, under the conditions of low pH with addition of 0.15 to 0.3
kg/tDS, the α-amylase variant was still able to normally liquefy, indicating that
the α-amylase variant was highly tolerant to low pH, and at the same time, under condition
of a small amount of enzyme added of 0.15 kg/tDS, the α-amylase variant of the present
invention was still able to normally liquefy, which could effectively reduce the cost
for enzyme used in factories.
[0090] In addition, we performed a test for the effect of α-amylase variant on saccharification
and compared it with a liquefaction solution liquefied with Liquozyme Supra (purchased
from Novozymes). Test conditions: 32% dry matter (DS), well-mixed, pH adjusted to
4.3 with hydrochloric acid. 0.45 kg/tDS complex glucoamylase was added and the reactions
of 200 ml were conducted at 60°C for 24 and 48 hours, respectively. Samples were filtered
by 0.22 µm membrane and inactivated at 100°C for HPLC analysis. The results are shown
in Table 4.
Table 4: Effect of the α-amylase variant on saccharification
| Amylase |
Glucose % |
| 24 hrs |
48 hrs |
| α-amylase variant |
95.11 |
96.4 |
| Liquozyme Supra |
95.55 |
96.38 |
[0091] As shown in Table 4, the liquefaction solution of the α-amylase variant and the liquefaction
solution of Liquozyme Supra had the same saccharification effect, indicating that
the α-amylase variant could be applied to the starch sugar industry.
[0092] Finally, because α-amylase has important applications in the alcohol industry, we
have also tested the liquefaction effect of this α-amylase variant on alcohol production.
Corn flour (40 mesh) with a ratio of feed to water of 1:2.5 was prepared, the pH was
adjusted to 5.8 with hydrochloric acid, and 0.145 kg/t DS of the α-amylase variant
was added. The solution was liquefied at 95°C for 120 min. After the reaction was
completed, the DE and the viscosity of the sample were measured, and a comparative
test with Liquzoyme SC (available from Novozymes) was also conducted at the same time.
The results are shown in Table 5.
Table 5: Comparison of application of α-amylase variant in corn alcohol liquefaction
| Amylase |
DE (%) |
viscosity (mPas) |
| α-amylase variant |
10.02 |
11650 |
| Liquozyme SC |
10.05 |
11710 |
[0093] As shown in Table 5, the α-amylase variant could achieve the same application effect
as Liquzoyme SC, indicating that it could be applied to the corn alcohol industry.
[0094] In summary, according to the experimental results in the present invention, the series
of α-amylase variants had better heat resistance and pH tolerance, and could be applied
to the liquefaction of high-strength starch slurry, and thus could be applied to the
starch sugar industry and the alcohol industry.
[0095] The examples of the present invention are inseparable from the teachings of the present
invention in addition to the technical means in the art. Therefore, the invention
is not limited to the specific examples disclosed, but also to additional modifications
within the spirit and scope of the invention, as described in details in the appended
claims.
1. An α-amylase variant, which is obtained by mutating or deleting at least one amino
acid residue in amino acid sequence of a parental α-amylase while still retaining
the ability of the parental α-amylase to hydrolyze an α-1,4 glycosidic bond; and has
amino acid sequence homology of 95% or more with the parental α-amylase.
2. The α-amylase variant according to claim 1, wherein the parental α-amylase is a bacterial
α-amylase of any one selected from the group consisting of Bacillus subtilis, B. licheniformis, B. amyloliquefaciens, G. stearothermophilus or Bacillus cereus.
3. The α-amylase variant according to claim 2, wherein the parental α-amylase is an α-amylase
of B. licheniformis or G. stearothermophilus, preferably an α-amylase of G. stearothermophilus.
4. The α-amylase variant according to claim 3, wherein the full-length gene coding sequence
of the α-amylase of G. stearothermophilus is set forth in SEQ ID NO: 1; and the corresponding amino acid sequence is set forth
in SEQ ID NO: 2.
5. The α-amylase variant according to claim 4, wherein the α-amylase variant is obtained
by any one of the following or any combination of the following:
(1) deleting the 1st to 5th amino acid residues from the N-terminus of the parental α-amylase of G. stearothermophilus and replacing with VN or ANLN;
(2) deleting 27 to 32 amino acid residues from the C-terminus of the parental α-amylase
of G. stearothermophilus;
(3) deleting the 180th and 181st amino acid residues from the N-terminus of the parental α-amylase of G. stearothermophilus.
6. The α-amylase variant according to claim 5, wherein the C-terminus of the α-amylase
variant is added with three amino acid residues of FAN.
7. The α-amylase variant according to claim 5 or 6, wherein the amino acid sequence of
the α-amylase variant is any one selected from the group consisting of SEQ ID NO:
4, SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 10 and SEQ ID NO: 12.
8. The α-amylase variant according to claim 7, wherein the nucleotide coding sequence
of the α-amylase variant is any one selected from the group consisting of SEQ ID NO:
3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9 and SEQ ID NO: 11.
9. A gene encoding the α-amylase variant according to any one of claims 1 to 6.
10. The gene according to claim 9, wherein the nucleotide sequence of the gene is any
one selected from the group consisting of SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7,
SEQ ID NO: 9 and SEQ ID NO: 11.
11. An expression vector for expressing the α-amylase variant according to any one of
claims 1 to 6, wherein the expression vector comprises the gene encoding the α-amylase
variant according to claim 8.
12. The expression vector according to claim 11, wherein the expression vector comprises
an expression cassette mainly comprised of a natural or synthetic promoter sequence,
a natural or synthetic ribosome binding site, a natural or synthetic terminator sequence,
and the gene encoding the α-amylase variant according to claim 8.
13. A recombinant cell for expressing the α-amylase variant according to any one of claims
1 to 6, comprising one or more of the genes encoding the α-amylase variant according
to claim 9.
14. The recombinant cell according to claim 13, wherein the host cell of the recombinant
cell is selected from a Bacillus strain, preferably B. licheniformis, or a Bacillus strain genetically engineered to inactivate some endogenous proteins.
15. The recombinant cell according to claim 14, wherein the host cell of the recombinant
cell is selected from B. licheniformis genetically engineered to inactivate AprE and/or NprE.
16. A method for producing the α-amylase variant according to any one of claims 1-6, comprises
culturing a recombinant cell comprising a gene sequence encoding the α-amylase variant
under conditions suitable for the expression of the α-amylase variant, and the α-amylase
variant is obtained from the recombinant cell or its culture supernatant.
17. Use of the α-amylase variant according to any one of claims 1-6 in hydrolysis of an
α-1,4 glycosidic bond of a polysaccharide.
18. The use according to claim 17, wherein the α-amylase variant is used in the hydrolysis
of an α-1,4 glycosidic bond of a polysaccharide under conditions of a high temperature
and/or a low pH, wherein the high temperature is preferably 80°C to 110°C, more preferably
100°C to 110°C; the low pH is preferably 5.0 to 5.5.